Process for making repulpable corrugated box

ABSTRACT

A repulpable moisture resistant poultry box having a composite structure with a fluted medium, a top backing board secured to one side of the fluted medium and a bottom backing board secured to the other side of the fluted medium. The backing boards and the fluted medium are impregnated with a hydrogenated triglyceride. The backing boards each have an outer surface coated with an emulsion of hydrogenated triglyceride and styrene acrylic to provide moisture resistance repulpable and recyclable box.

RELATED APPLICATIONS

This is a divisional application of U.S. patent application Ser. No. 13/815,398 filed Feb. 28, 2013 which is a continuation-in-part application of U.S. patent application Ser. No. 12/320,429 filed Jan. 26, 2009.

STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT

Not applicable.

REFERENCE TO SEQUENCE LISTING, A TABLE, OR A COMPUTER PROGRAM LISTING COMPACT DISC APPENDIX

None.

FIELD OF THE INVENTION

The present invention generally relates to moisture resistant and water proof paper products including linerboard and corrugated board. Particularly, this invention relates to moisture resistant paper boxes used primarily in the poultry industry that are waterproofed and can be repulped and recycled to be part of the feedstock for new paper products that minimizes environmental concerns.

BACKGROUND OF THE INVENTION

In the manufacture of paper and paperboard and of products made from same, petroleum derived paraffin waxes and synthetic polymers have been used for many years as moisture retardants, water repellents, oil repellents, stiffeners, strengtheners, and release agents. Besides paraffin, the material used most often in such products is polyethylene. However, other widely used polymers in the field include polymerized acrylics, vinyls, styrenes, ethylenes and copolymers or hetero-polymers of these monomers. The paper and paperboard to which these traditional materials are applied is difficult and often impossible to repulp and recycle in standard paper mill processes because the petroleum derived polymers and, particularly, the petroleum waxes are non-biodegradable in mill white waters (circulated process waters) and discharge effluents. Furthermore, the residue of the petroleum waxes that is not removed from pulp fibers during the repulping and recycling processes causes severe problems due to buildup that occurs on the screens and felts used during the process of forming and making the paper or paperboard sheet. In addition, paper and paperboard coated or impregnated with petroleum waxes resist biodegradation and composting when disposed of in landfills and other waste disposal systems. Paper and paperboard coated or impregnated with traditional synthetic polymers and hetero-polymers are also difficult and often impossible to repulp and recycle owing to their resistance to separation from the fiber in the standard repulping processes resulting in significant fiber losses in efforts to repulp and recycle them, and these are also non-biodegradable and therefore resist composting.

Water repellent packaging currently utilizes petroleum based liquid polymers or polymer film laminates (including polyethylene or similar film laminates such as polyolefin, polyester, polyvinyl alcohol, polyvinyl acetate, polystyrene, polypropylene, and the like) which are recyclable after extensive treatment, All of these laminates require the installation of specialized repulping machinery that separates the pulp fibers from the laminated films and/or is far more expensive in terms of operating costs and/or recycled pulp fiber yields. The action of separating the fiber from the film damages some fibers causing them to be selected out of the recycled pulp and presented for reuse, and the separated film waste carries some of the fibers out of the repulpate when its adherence is not interrupted by the repulping process. Likewise, coatings and impregnating products made from or based on paraffin waxes and/or similar petroleum derivatives can be repulped for recycling in specially configured repulping equipment that removes and separates the paraffin waxes; however, as in the laminated film repulping process, the more intense physical and chemical requirements of this repulping process coupled with the lost fibers that become trapped in paraffin wax wastes cause the recyclable repulped fiber levels to fall far below those of standard repulping processes. Moreover, boxes made from such products are not biodegradable and must be separated and deposited in separate landfill areas.

The poultry box industry currently uses a wax to coat the boxes (EVA—poly (ethylene vinyl acetate) which takes a significantly long period of time to compost and leaves a chemical residue from those compounds. There appears to be little or no decomposition of higher molecular weight resin and EVA fractions.

In the prior art, a number of patents have attempted to address the above noted problem. U.S. Pat. No. 6,103,308 issued Aug. 15, 2000 is directed toward a paper and paperboard coating composition using vegetable oil triglyceride as a paper coating while U.S. Pat. No. 6,201,053 issued Mar. 13, 2001 is directed toward various triglycerides mixed with catalysts for use as a waterproofing agent on paper coating.

U.S. Pat. No. 6,846,573 issued Jan. 25, 2005 discloses the use of hydrogenated triglycerides having a melting point above 50° as a coating material for the surface of paper products to improve wet strength and moisture resistance in addition to being repulpable.

The use of tallow to treat paper is also well known in the prior art. U.S. Pat. No. 2,840,138 issued Jun. 24, 1958 discloses the use of tallow fatty acids to impregnate and penetrate corrugated paper material to provide a wilt resistant material. Also, U.S. Pat. No. 4,752,637 issued Jun. 21, 1988 is directed to a method of treating fiberboard to have superior moisture resistance with various mixtures of hydroxy terminated esters such as tallow.

None of the noted references have provided a repulpable, recyclable corrugated box capable of holding iced products and being moisture resistant.

SUMMARY OF THE INVENTION

The present invention is directed to a backed corrugated paper box product which has the outer paper liner or backer sheet surfaces coated with a homogenized styrene/acrylic hydrogenated triglyceride emulsion with the inner corrugated paper medium and liner sheets being impregnated with a hydrogenated triglyceride such as tallow.

Hydrogenated tallow triglycerides can be applied in the same manner as the traditional petroleum waxes and synthetic polymers and function as moisture retardants, water repellents, oil repellents, stiffeners, strengtheners, and release agents in the manufacture of paper, paperboard, packaging, molding forms, and other common applications. A particular advantage is that such hydrogenated tallow triglycerides are readily biodegradable in paper mill white waters and is compostable in landfill or other waste disposal systems. The present invention is easier to repulp and recycle without detriment to production equipment, processes, or manufactured product quality or performance.

It is an object of this invention to produce a paper product which can be repulped and recycled.

It is another object of the invention to provide a poultry box which is biodegradable. It is still another object of the invention to provide a poultry box which has superior moisture resistance.

The invention will be better understood and objects other than those set forth above will become apparent when consideration is given to the following detailed description thereof Such description makes reference to the annexed drawings wherein.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic of the process used in making the poultry box composite material;

FIG. 2 is a top plan view of the inventive poultry box invention; and

FIG. 3 is an enlarged cross sectional view of the inventive poultry box invention.

DETAILED DESCRIPTION OF THE INVENTION

The preferred embodiments and best mode of the invention are shown in FIGS. 1 through 3. While the invention is described in connection with certain preferred embodiments, it is not intended that the present invention be so limited. On the contrary, it is intended to cover all alternatives, modifications, and equivalent arrangements as may be included within the spirit and scope of the invention as defined by the appended claims.

Definitions

As used herein the following abbreviations and terms are understood to have the meanings as set forth:

“Triglyceride” includes both animal fats and vegetable oils and is derived from one or both of them. Animal fats include beef tallow, pork lard, poultry grease and fish oils. Vegetable oils include soybean oil, peanut oil, olive oil, palm oil, coconut oil and cottonseed oil.

“Paraffin” is a wax-like product derived from petroleum.

“Paper” includes substrates and surfaces of cellulosic material.

It has been found that hydrogenated triglycerides and preferably lard or tallow triglycerides can be substituted for petroleum based paraffin waxes and wax compounds in the manufacturer of paper products. All of these application systems involve melted triglycerides held at temperatures in the range from around 125° F. to 170° F. which is either squeezed, rolled, cascaded, sprayed, or doctored onto the linerboard, paper, carton stock, or corrugated medium surface to impregnate the same.

The method and machinery or equipment for repulping and recycling scrap paper in the paper and paperboard or liner board industry is both an established and well known art, and the equipment required is standard and commonly installed at most mills incorporating recycled paper in their manufacturing feed stocks. Thus, those skilled in the paper making art are also knowledgeable in re-pulping and recycling.

Poultry boxes are unique paper products that need to withstand water and poultry fluid. The present inventive poultry box is made of double backer corrugated board having a corrugated medium of 30 to 40 lb./1000 sq. ft. (MSF) paperboard of an “A”, “B”, “C”, “E” and “F” flute size (weight depends upon various external factors). The preferred flute size used in the invention is an “A” flute having 33+/−3 flutes per lineal foot with a flute thickness of 3/8 inch or a “C” flute having 39+/−3 flutes per lineal foot with a flute thickness of 5/32 inch. A flat liner or backer board of Kraft paper (various grades) is adhered to one side of the fluted medium with a starch based adhesive and a second flat liner or backer board of Kraft paper is adhered to the other side of the fluted medium with a starch based adhesive to form a backed corrugated board. The Kraft paperboard liner may be bleached white, coated white (white coat), mottled white or colored. As is well known in the art, the medium paper is humidified by means of high pressure steam which softens the paper fibers to facilitate the formation of the flute and consequent gluing. After formation of the board, this humidity is removed by drying in the dry-end. In the present invention, the newly formed corrugated liner board is heated from the bottom by hot plates and the adhesive holding components of the structure is cured.

The present repulpable inventive degradable poultry box 10 is constructed with an inner Kraft paper liner or backer 12 impregnated with a hydrogenated triglyceride, preferably tallow at 2.5 lbs/MSF, a corrugated paper medium 14 impregnated with a hydrogenated triglyceride, preferably tallow at 3.5 lbs/MSF and the outer Kraft paper liner or backer 16 is impregnated with tallow at 2.5 lbs/MSF. Other triglycerides can be used such as animal fats and vegetable oils. Animal fats include beef tallow, pork lard, poultry grease and fish oils. Vegetable oils include soybean oil, peanut oil, olive oil, palm oil, coconut oil and cottonseed oil. Tallow used in the impregnation is commercially available from C.J. Robinson Co. and Chemol Corporation. After tallow impregnation of the paper liners, both liners or backers 16 are coated on their outside surfaces with a coating 18 of a styrene acrylic co-polymer water based solution ranging from about 75% to about 95% by weight mixed or blended with hydrogenated triglyceride preferably in the nature of tallow ranging from about 5% to about 25% by weight to form an emulsified coating. A most preferred embodiment of the coating 18 is about 80% by weight styrene acrylic co-polymer solution and about 20% by weight hydrogenated triglyceride which is preferably in the form of tallow. The coating emulsion is heated and mixed at the general time of application and heated to a temperature from about 160° F. to about 180° F., preferably at 170° F.

The coating 18 is a water based high solid fluid solution (% by weight of the styrene acrylic co-polymer ranging from about 50% to about 55%) most preferably about 52% and has a pH ranging from about 8-9 with fully cured Tg of +7, a specific gravity of ranging from about 1.04 to about 1.6 and viscosity (cps) of about 400, a vapor density the same as water with 30 minute Cobb values of 10 or better. The coating is fast drying, recyclable, repulpable and is printable and glueable.

The present poultry box 10 is constructed using standard corrugated box making machinery as is well known in the art. A roll of the medium paper 30 is positioned upstream of the corrugator. The paper is wetted and passed through a standard corrugating machine 35 and formed into a corrugated medium 32 having the desired flute size, preferably “A” or “C”. The corrugated medium 32 is transported downstream through a tallow bath 36 and rollers with the corrugated medium being impregnated with tallow at 2.5 to 3.5 lbs/MSF. The impregnated corrugated medium 37 is carried by belts to an assembly station 60 where the coated liner backers 45 and 55 as further described below are secured to the corrugated medium 37 to form a composite sheet poultry box carton blank. Two liner rolls of roll stock of Kraft paper 40 and 50 are removed from the respective rolls and the respective liner sheets 41 and 51 are transported by rollers through separate hydrogenated triglyceride, preferably tallow baths 42 and 52 and their associated rollers which applies tallow to the liner backer sheets 41 and 51 at 2.5 lbs/MSF impregnating the same. The now impregnated liner backer sheets 43 and 53 are then transported by rollers to and coated at coating stations 44 and 54 on a single sheet surface side with the emulsion coating 18 heated to about 170° F. The emulsion coating can be placed on the sheet backing surface by rollers, doctor blades or spraying as is well known in the art. The coating is translucent to milky white and is water based. The coated liner sheets 45 and 55 are then glued at gluing station 60 to the corrugated medium 37 with a suitable adhesive as is well known in the art to form a coated corrugated composite board with emulsified coating 18 on its top and bottom outside surfaces. The coated corrugated composite board 61 is then passed over a heat curing bed 70 to cure and set the adhesive or glue. The heat curing bed 70 is a series of hot plates and pressure rollers which applies light pressure and heat to cure the adhesive which is standard in the corrugated box making art and the glue cures very rapidly. The composite board is run through a chill plate assembly 80 which drops the corrugated temperature 70° F. allowing the blanks to be stacked without sticking. The composite corrugated board sheet 61 is then cut into individual blank sections in a cutting and stacking station 90 with known means stacking the individual flat sheets of composite corrugated board. If desired, air impact dryers 100 can be used to dry the flat sheets. The individual composite corrugated blanks are stacked and dried for a day. The blanks are later placed in a standard box cutting station which cuts and scores the composite poultry box 10 in the form shown in FIG. 2.

The poultry boxes are then delivered and assembled at the poultry packing plant and an adhesive provided by the manufacturer is placed vertically along the poultry box to provide a structurally sound moisture proof poultry box 10.

The principles, preferred embodiments and modes of operation of the present invention have been described in the foregoing specification. However, the invention should not be construed as limited to the particular embodiments which have been described above. Instead, the embodiments described here should be regarded as illustrative rather than restrictive. Variations and changes may be made by others without departing from the scope of the present invention as defined by the following claims: 

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 13. A process for making a repulpable and recyclable poultry box comprising the steps of: a). impregnating a corrugated paper medium with hydrogenated triglyceride; b). impregnating a first paper liner board with hydrogenated triglyceride; c). impregnating a second paper liner board with hydrogenated triglyceride; d). coating said impregnated first paper liner board with a coating of emulsified styrene acrylic co-polymer and hydrogenated triglyceride on one side; e). coating said impregnated second paper liner board with a coating of emulsified styrene acrylic co-polymer and hydrogenated triglyceride on one side; f). securing said first impregnated and coated liner board, said impregnated corrugated medium and said second impregnated and coated liner board together with the corrugated medium in the middle with an adhesive to form a composite sheet; and g). curing said composite sheet with heat to cure said adhesive.
 14. A process as claimed in claim 13 wherein said hydrogenated triglyceride ranges from about 5% to about 25% by weight of the coating.
 15. A process as claimed in claim 13 wherein said coating of emulsified styrene acrylic co-polymer and hydrogenated triglyceride is in a water solution and said styrene acrylic co-polymer ranges from about 50% to about 55% by weight of the solution.
 16. A process as claimed in claim 13 wherein said hydrogenated triglyceride is tallow, said tallow comprising about 20% by weight of the coating.
 17. A process as claimed in claim 13 wherein the hydrogenated triglyceride is an animal fat selected from one or more of a group consisting of beef tallow, pork lard, poultry grease, and fish oils.
 18. A process as claimed in claim 13 wherein the hydrogenated triglyceride is a hydrogenated vegetable oil selected from one or more of a group consisting of soybean oil, peanut oil, olive oil, palm oil, coconut oil and cottonseed oil.
 19. A process for making a repulpable and recyclable poultry box as claimed in claim 13 including the additional step of: h). cooling the composite sheet causing a temperature drop of said composite sheet to at least 70° F.
 20. A process for making a repulpable and recyclable poultry box as claimed in claim 19 including an additional step after step h) of: i). cutting the composite sheet into box blanks.
 21. A process for making a repulpable and recyclable poultry box in an inline corrugating machine comprising the steps of: a). impregnating a corrugated paper medium with hydrogenated triglyceride; b). impregnating a first paper liner board with hydrogenated triglyceride; c). impregnating a second paper liner board with hydrogenated triglyceride; d). coating said impregnated first paper liner board with a coating of emulsified styrene acrylic co-polymer and hydrogenated triglyceride in a water solution on one side; e). coating said impregnated second paper liner board with a coating of emulsified styrene acrylic co-polymer and hydrogenated triglyceride in a water solution on one side; f). securing said first impregnated and coated liner board, said impregnated corrugated medium and said second impregnated and coated liner board together with said impregnated corrugated medium in the middle with an adhesive to form a composite sheet; g). curing said composite sheet with heat to cure said adhesive; and h). cooling said composite sheet to a suitable temperature to allow cutting and stacking.
 22. A process as claimed in claim 21 wherein the hydrogenated triglyceride is an animal fat selected from one or more of a group consisting of beef tallow, pork lard, poultry grease, and fish oils.
 23. A process as claimed in claim 21 wherein the hydrogenated triglyceride is a hydrogenated vegetable oil selected from one or more of a group consisting of soybean oil, peanut oil, olive oil, palm oil, coconut oil and cottonseed oil.
 24. A process for making a repulpable and recyclable poultry box as claimed in claim 21 wherein said cooling step: includes cooling the composite sheet until it reaches a temperature of about 70° F.
 25. A process for making a repulpable and recyclable poultry box as claimed in claim 21 including an additional step i) of: i). cutting the cooled composite sheet into blanks.
 26. A process as claimed in claim 21 wherein said hydrogenated triglyceride is tallow ranging from about 5% to about 25% by weight of the coating.
 27. A process as claimed in claim 21 wherein said styrene acrylic co-polymer ranges from about 50% to about 55% by weight of the solution.
 28. A process as claimed in claim 21 wherein said hydrogenated triglyceride is tallow and is about 20% by weight of the coating.
 29. A process for making a repulpable and recyclable poultry box in an inline corrugating machine comprising the steps of: a). impregnating a corrugated paper medium with tallow; b). impregnating a first paper liner board with tallow; c). impregnating a second paper liner board with tallow; d). coating said impregnated first paper liner board with a coating of emulsified styrene acrylic co-polymer and tallow in a water solution on one side; e). coating said impregnated second paper liner board with a coating of emulsified styrene acrylic co-polymer and tallow in a water solution on one side; f). securing said first impregnated and coated liner board, said corrugated medium and said second impregnated and coated liner board together with glue with the corrugated medium positioned between said first and second impregnated and coated liner board to form a composite sheet; g). curing said composite sheet with heat to cure said glue; h). cooling said composite sheet until it reaches about ambient temperature; and i). cutting said dried composite sheet into blanks and stacking said blanks.
 30. A process as claimed in claim 29 wherein said tallow ranges from 5% to about 25% by weight of the coating and said styrene acrylic co-polymer ranges from about 75% to about 95% by weight of the coating.
 31. A process as claimed in claim 29 wherein said corrugated paper medium ranges from about 30 pounds to about 40 pounds per 1000 sq. ft. (MSF).
 32. A process as claimed in claim 29 wherein said first and second liner board is impregnated with tallow at about 2.5 lbs./MSF. 